Synthesis of Sucrose Fatty Acid Esters by Using Mixed
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Sucrose Octanoate Esters Crop 1 2 Identification of Petitioned Substance
Sucrose Octanoate Esters Crop 1 2 Identification of Petitioned Substance 3 Chemical Names: CAS Numbers: 4 sucrose octanoate esters 15 CAS NO. 42922-74-7 (monooctanoate), 58064-47-4 5 16 (dioctanoate) 6 Other Name: 7 (∀-D-glucopyranosyl-∃-D-fructofuranosyl- Other Codes: 8 octanoate), mono-, di-, and triesters of sucrose 17 OPP Chemical Code: 035300 9 octanoate 10 11 Trade Names: 12 Avachem Sucrose Octanoate Manufacturing Use 13 Product 14 Avachem Sucrose Octanoate [40%] 18 19 Characterization of Petitioned Substance 20 21 Composition of the Substance: 22 23 Sucrose octanoate esters (SOEs) belong to the organic chemical family sucrose fatty acid esters (SFAEs).1 24 SFAEs are surfactants (or surface active agents) that lower the surface tension of a liquid, allowing easier 25 spreading and evaporation. Surfactants are usually organic compounds that contain both hydrophobic 26 (fat-soluble) and hydrophilic (water-soluble) groups (Wikipedia, n. d.). SFAEs have sucrose residues as the 27 hydrophilic group and fatty acid residues as the lipophilic group. SOEs are manufactured from sucrose 28 (table sugar) and an octanoic acid ester commonly found in plants and animals. Sucrose esters, as a class of 29 related compounds, vary depending on the number and locations of esters attached to the sucrose 30 molecules. Sucrose has eight potential places where individual esters may attach (Montello Inc., n. d.). The 31 substance under review is a mixture of mono-, di-, and triesters. 32 33 Sucrose esters were first isolated when researchers investigated the insecticidal properties of the tobacco 34 leaf hairs. This insecticidal property of sucrose esters acts by dissolving the waxy protective coating 35 (cuticle) of target pests, causing them to dry out and die (U.S. -
Sucrose Esters in Gel-To-Milk Emulsion Concepts
For know-how in sucrose ester techniques Sucrose esters in gel-to-milk emulsion concepts EXPERIENCE OUR EXPERTISE! Introduction Sisterna B.V.is a young and flexible organisation that is solely active in the promotion and sales of Sisterna® sucrose esters. Furthermore Sisterna has developed countless proven and innovative applications of these natural and multifunctional emulsifiers for the cosmetic industry. Sisterna® sucrose esters are based on sucrose and vegetable fatty acids and are a unique range of high quality, non-ionic emulsifiers with an exceptional performance and mildness to skin and eyes. Besides emulsification Sisterna® sucrose esters can offer other unique benefits to personal care formulations. Sisterna has developed various interesting emulsion concepts, such as a gel-to-milk concept, the subject of this paper. Sisterna’s exclusive distributor network ensures the availability and technological knowhow of sucrose esters in personal care applications in the Western Hemisphere. 2 Summary Sisterna® sucrose esters with a high HLB are very suitable emulsifiers for the development of natural 'oil gels' that turn into milk when diluted upon use. These 'oil gels' are in fact concentrated oil-in-glycerin (O/G) emulsions that can be produced by using standard high shear homogenising equipment. Very narrow oil droplet size emulsions with average oil droplet sizes of 300 - 500 micron are obtained. By using just 2% of one single high HLB sucrose ester, preferably sucrose palmitate, it is already possible to produce a gel-to-milk concept containing 60% of oil. Such a concept is very suitable for make-up cleansing. The high oil content will allow to remove all impurities. -
Effects of Selected Polysorbate and Sucrose Ester Emulsifiers on the Physicochemical Properties of Astaxanthin Nanodispersions
Molecules 2013, 18, 768-777; doi:10.3390/molecules18010768 OPEN ACCESS molecules ISSN 1420-3049 www.mdpi.com/journal/molecules Article Effects of Selected Polysorbate and Sucrose Ester Emulsifiers on the Physicochemical Properties of Astaxanthin Nanodispersions Navideh Anarjan 1,2 and Chin Ping Tan 1,* 1 Department of Food Technology, Faculty of Food Science and Technology, Universiti Putra Malaysia, 43400 UPM Serdang, Selangor, Malaysia; E-Mail: [email protected] 2 Young Researchers and Elites Club, East Azarbaijan Science and Research Branch, Islamic Azad University, 15655/461, Tabriz, Iran * Author to whom correspondence should be addressed; E-Mail: [email protected]; Tel.: +603-8946-8418; Fax: +603-8942-3552. Received: 7 December 2012; in revised form: 28 December2012 / Accepted: 31 December 2012 / Published: 9 January 2013 Abstract: The effects of selected nonionic emulsifiers on the physicochemical characteristics of astaxanthin nanodispersions produced by an emulsification/evaporation technique were studied. The emulsifiers used were polysorbates (Polysorbate 20, Polysorbate 40, Polysorbate 60 and Polysorbate 80) and sucrose esters of fatty acids (sucrose laurate, palmitate, stearate and oleate). The mean particle diameters of the nanodispersions ranged from 70 nm to 150 nm, depending on the emulsifier used. In the prepared nanodispersions, the astaxanthin particle diameter decreased with increasing emulsifier hydrophilicity and decreasing carbon number of the fatty acid in the emulsifier structure. Astaxanthin nanodispersions with the smallest particle diameters were produced with Polysorbate 20 and sucrose laurate among the polysorbates and the sucrose esters, respectively. We also found that the Polysorbate 80- and sucrose oleate-stabilized nanodispersions had the highest astaxanthin losses (i.e., the lowest astaxanthin contents in the final products) among the nanodispersions. -
Chemistry and New Uses of Sucrose: How Important?
Pure & Appi. Chem., Vol. 56, No. 7, pp. 833—844, 1984. 0033—4545/84 $3.OO+O.OO Printed in Great Britain. Pergamon Press Ltd. ©1984 IUPAC CHEMISTRY AND NEW USES OF SUCROSE: HOW IMPORTANT? Riaz Khan Philip Lyle Memorial Research Laboratory, Tate & Lyle PLC, Whiteknights P.O. Box 68, Reading, England Abstract —Somerecent work on selective reactions of sucrose is described. These reactions reveal a profile of chemical reactivity which has been exploited to produce a number of products of commercial significance. The potential of sucrose as a raw material for chemicals and energy is also indicated. INTRODUCTION The world economy is critically dependent upon oil which is a non—regenerable material. In order to maintain an economic order in the world it is therefore imperative that the future energy and chemical needs are secured. In the short—term we must curb on wasteful consumption of oil and in the long—term dependence on oil must be reduced. Alternative resources such as coal, tarsands, shale oil, natural gas and lignite, agricultural and aquatic materials must be considered as sources of energy and chemicals. The potential of carbohydrates as feedstocks for chemicals has been demonstrated, but not yet significantly commercially realised except in a few instances. Although cellulose is the most abundant carbohydrate, several technical difficulties in its processing makes it economically unattractive as a raw material for energy and chemicals. In contrast sucrose and starch are readily amenable to chemical and biochemical modifications giving a range of compounds presently derived through petrochemical routes, as well as new derivatives of potential commercial significance. -
Natured Alcohol and Spe- Cially Denatured
Alcohol and Tobacco Tax and Trade Bureau, Treasury § 21.141 (c) Purity. Technical grade or better. droxide. Reflux for 1 hour on a steam bath, cool and titrate the excess so- [T.D. ATF–133, 48 FR 24673, June 2, 1983. Re- designated by T.D. ATF–442, 66 FR 12854, dium hydroxide with 0.5 N sulfuric acid Mar. 1, 2001] using phenolphthalein indicator. Percent sucrose octaacetate=(ml NaOH¥ml § 21.129 Spearmint oil, terpeneless. H2SO4)×4.2412/weight of sample (a) Carvone content. Not less than 85 percent by weight. [T.D. ATF–133, 48 FR 24673, June 2, 1983. Re- ° designated by T.D. ATF–442, 66 FR 12854, (b) Refractive index at 20 C. 1.4930 to Mar. 1, 2001] 1.4980. (c) Specific gravity at 25 °/25 °C. 0.949 to § 21.132 Toluene. 0.956. (d) Odor. Characteristic odor. (a) Distillation range. (For applicable ASTM method, see 1980 Annual Book of [T.D. ATF–133, 48 FR 24673, June 2, 1983. Re- ASTM Standards, Part 29, page 569, designated by T.D. ATF–442, 66 FR 12854, Standard No. D 362–75 for industrial Mar. 1, 2001] grade toluene; for incorporation by ref- § 21.130 Spike lavender oil, natural. erence, see § 21.6(b).) When 100 ml of tol- uene are distilled by this method, not (a) Alcohol content (as borneol). Not more than 1 ml should distill below 109 less than 30 percent by weight. °C., and not less than 99 ml below 112 (b) Esters (as bornyl acetate). Not less °C. than 1.5 percent by weight. -
SDS Contains All of the Information Required by the HPR
SAFETY DATA SHEET Preparation Date: 01/26/2015 Revision Date: 7/25/2018 Revision Number: G2 1. IDENTIFICATION Product identifier Product code: SU104 Product Name: SUCROSE OCTAACETATE, NF Other means of identification Synonyms: alpha-d-glucopyranoside; 1,3,4,6-tetra-O-acetyl-beta-D-Frutofuranosyl; tetraacetate; Octaacetylsucrose CAS #: C28H38O19 RTECS # WN6620000 CI#: Not available Recommended use of the chemical and restrictions on use Recommended use: No information available. Uses advised against No information available Supplier: Spectrum Chemical Mfg. Corp 14422 South San Pedro St. Gardena, CA 90248 (310) 516-8000 Order Online At: https://www.spectrumchemical.com Emergency telephone number Chemtrec 1-800-424-9300 Contact Person: Martin LaBenz (West Coast) Contact Person: Ibad Tirmiz (East Coast) 2. HAZARDS IDENTIFICATION Classification This chemical is not considered hazardous according to the 2012 OSHA Hazard Communication Standard (29 CFR 1910.1200) Not a dangerous substance or mixture according to the Globally Harmonized System (GHS) Label elements Not classified Hazards not otherwise classified (HNOC) Not Applicable Other hazards Not available Product code: SU104 Product name: SUCROSE 1 / 10 OCTAACETATE, NF 3. COMPOSITION/INFORMATION ON INGREDIENTS Components CAS-No. Weight % Sucrose Octaacetate 126-14-7 100 4. FIRST AID MEASURES First aid measures General Advice: National Capital Poison Center in the United States can provide assistance if you have a poison emergency and need to talk to a poison specialist. Call 1-800-222-1222. Skin Contact: Wash off immediately with soap and plenty of water removing all contaminated clothing and shoes. Get medical attention if irritation develops. Consult a physician if necessary. -
Process for the Production of a Surfactant Containing Sucrose Esters
Patentamt JEuropaischesEuropean Patent Office © Publication number: 0 031 191 Office europeen des brevets A1 © EUROPEAN PATENT APPLICATION © Application number: 80302785.3 © Int. CI.3: C 07 H 15/06 © Date of filing: 13.08.80 © Priority: 19.12.79 GB 7943762 © Inventor: Galleymore, Harry Reginald 01.05.80 GB 8014370 69 High Street Bathford Bath BA1 7SZAvon(GB) © Date of publication of application: (72) Inventor: James, Kenneth 01.07.81 Bulletin 81/26 34, Crawford Close Earley Reading Berkshire(GB) © Designated Contracting States: AT BE CH DE FR IT LI LU NL SE ©) Inventor: Jones, Haydn Frederick 27, Malone Road Woodley © Applicant: TATE & LYLE PATENT HOLDINGS LIMITED Reading Berkshire(GB) 5th Floor, Triningham Building Front Street Hamilton 5(BM) © Inventor: Bhardwaj, Chaman Lai 31 Crescent Road Tilehurst © Applicant: TALRES DEVELOPMENT (N.A.) N.V. Reading Berkshire RG3 5AH(GB) Breedestraat 39C Curacao, Netherlands Antiiles(NL) (72) Inventor: Plant, James Stephen Deceased © Designated Contracting States: G(GB) BE © Representative: Ablewhite, Alan James et al, MARKS & CLERK 57/60 Lincoln's Inn Fields London WC2A3LS(GB) © Process for the production of a surfactant containing sucrose esters. The process for the preparation of a surfactant mixture containing sucrose mono-and di-esters, by reacting a starting mixture including solid particulate sucrose, at least one trig- lyceride of a fatty acid having at least 8 carbon atoms and a basictransesterification catalyst, atatemperature offrom 110 to 140°C at atmospheric pressure and in the absence of any solvent, is improved by using a starting mixture which:- (a) contains a di and/or mono-glyceride in an amount to provide a hydroxyl value of greater than 500 mg KOH/100g of starting mixture; (b) contains at least 10% by weight of a fatty acid soap in addition to the basic transesterification catalyst, at least 50% by weight of the soap being potassium soap, and (c) (when the soap content is less than 20% by weight) contains at least 25% by weight of sucrose. -
Nanoemulsion Including Sucrose Fatty Acid Ester Nanoemulsionen Enthaltend Saccharosefettsäureester Nanoemulsions Comprenant Des Ester D’Acide Gras De Sucrose
(19) TZZ ¥__T (11) EP 2 563 164 B1 (12) EUROPEAN PATENT SPECIFICATION (45) Date of publication and mention (51) Int Cl.: of the grant of the patent: A23L 29/10 (2016.01) A23L 33/10 (2016.01) 29.06.2016 Bulletin 2016/26 A23L 33/15 (2016.01) A61K 9/107 (2006.01) (21) Application number: 11713391.8 (86) International application number: PCT/US2011/000538 (22) Date of filing: 22.03.2011 (87) International publication number: WO 2011/119228 (29.09.2011 Gazette 2011/39) (54) NANOEMULSION INCLUDING SUCROSE FATTY ACID ESTER NANOEMULSIONEN ENTHALTEND SACCHAROSEFETTSÄUREESTER NANOEMULSIONS COMPRENANT DES ESTER D’ACIDE GRAS DE SUCROSE (84) Designated Contracting States: (72) Inventor: BROMLEY, Philip, J. AL AT BE BG CH CY CZ DE DK EE ES FI FR GB Fullerton, CA 92832 (US) GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR (74) Representative: Boult Wade Tennant Designated Extension States: Verulam Gardens BA ME 70 Gray’s Inn Road London WC1X 8BT (GB) (30) Priority: 23.03.2010 US 340944 P (56) References cited: (43) Date of publication of application: WO-A1-2008/039564 WO-A1-2009/029046 06.03.2013 Bulletin 2013/10 WO-A1-2010/008762 DE-A1-102008 015 366 US-A1- 2009 297 665 (73) Proprietor: VIRUN, INC. Walnut, CA 91789 (US) Note: Within nine months of the publication of the mention of the grant of the European patent in the European Patent Bulletin, any person may give notice to the European Patent Office of opposition to that patent, in accordance with the Implementing Regulations. -
United States Patent (19) 11) 4,298,730 Galleymore Et Al
United States Patent (19) 11) 4,298,730 Galleymore et al. 45 Nov. 3, 1981 54 PROCESS FOR THE PRODUCTION OF A 3,867,301 2/1975 Watanabe............................ 252/132 SURFACTANT CONTAINING SUCROSE 3,963,699 6/1976 Rizzi............. ... 534/119 ESTERS 3,996,206 12/1976 Parker. 536/119 4,032,702 6/1977 James .................................. 536/119 75 Inventors: Harry R. Galleymore, Bath; Kenneth James, Reading; Haydn F. Jones, FOREIGN PATENT DOCUMENTS Reading; Chaman L. Bhardwaj, 1399053 6/1975 United Kingdom................ 536/119 Reading, all of England; James S. Plant, deceased, late of Reading, Primary Examiner-Dennis L. Albrecht England; by Aline P. Plant, Attorney, Agent, or Firm-Ostrolenk, Faber, Gerb & administrator, Manchester, England Soffen 73) Assignee: Tahres Development (N.A.) N.V., (57) ABSTRACT Curacao, Netherlands Antilles The process for the preparation of a surfactant mixture containing sucrose mono- and di-esters, by reacting a 21) Appl. No.: 174,277 starting mixture including solid particulate sucrose, at 22 Filed: Jul. 31, 1980 least one triglyceride of a fatty acid having at least 8 30 Foreign Application Priority Data carbon atoms and a basic transesterification catalyst, at a temperature of from 110 to 140° C. at atmospheric Dec. 19, 1979 (GB) United Kingdom ..... ... 43762/79 pressure and in the absence of any solvent, is improved May 1, 1980 GB United Kingdom ............... 14370/80 by using a starting mixture which: 51) Int. Cl. ....................... C07H 13/06; C11D 1/66; (a) contains a di and/or mono-glyceride in an amount C11D 9/26; C11D 11/04 to provide a hydroxyl value of greater than 500 mg 52) U.S. -
United States Patent Office Patented Apr
2,931,802 United States Patent Office Patented Apr. 5, 1960 1. 2 solved. Any unreacted anhydride and acid by-product are removed by distillation under reduced pressure. To re 2931,802 move traces of acid and the salt catalyst, the residue is dis solved in a water-immiscible inert solvent and the result MXED ESTERS OF GLUCOSE AND SUCROSE ing solution is washed with dilute NaOH or Na2CO3, George P. Touey and Herman E. Davis, Kingsport, Tenn., following which the aqueous layer is removed and the assignors to Eastman Kodak Company, Rochester, N.Y., inert solvent is distilled off under reduced pressure. Ordi a corporation of New Jersey narily, 2-3 hours gives sufficient time to run the reaction No Drawing. Application April 30, 1958 to completion although longer times. may be employed. Serial No. 731,890 10 If desired, an inert diluent may be employed in the esteri fication bath such as a ketonelike diethyl ketone, a hydro 7 Claims. (CI. 260-234) carbon such as toluene, or a chlorinated hydrocarbon such as propylene chloride. If a solvent is used its boil ing point should be within the range of 90-140 C. This invention relates to organic solvent soluble short 5 Acid diluents are preferably avoided since they may react chain fatty acid esters of sucrose and of glucose and with the anhydrides used, thereby altering the anhydride their method of preparation. In particular it relates to ratio employed. ... completely esterified or highly esterified mixed fatty acid To obtain non-crystallizing esters in accordance with esters of sucrose and glucose containing a combination of our invention the proportions of the combinations acetic acetyl and propionyl groups, or acetyl (or propionyl) and 20 anhydride-propionic anhydride, acetic anhydride-isobutyric isobutyryl groups as acyl substituents. -
Optimization of Ultrasound Synthesis of Sucrose Esters by Selection of a Suitable Catalyst and Reaction Conditions
JournalJournal of Chemical of Chemical Technology Technology and Metallurgy,and Metallurgy, 56, 2, 56, 2021, 2, 2021 268-274 OPTIMIZATION OF ULTRASOUND SYNTHESIS OF SUCROSE ESTERS BY SELECTION OF A SUITABLE CATALYST AND REACTION CONDITIONS Dragomir Vassilev1, Nadezhda Petkova2, Milena Koleva1, Panteley Denev2 1 Technical University of Gabrovo, 4 Hadji Dimitar str., 5300 Gabrovo, Bulgaria Received 25 October 2019 2 University of Food Technologies, 26 Maritza blv., 4002 Plovdiv, Bulgaria Accepted 10 January 2020 E-mail: [email protected] ABSTRACT Sucrose is used as a renewable raw material for the preparation of esters in various fields such as detergents, whitening boosters, cosmetics, medicines, nutritional supplements, emulsifiers, stabilizing agents, etc. By transes- terification of all hydroxyl groups with fatty acids, the polysubstituted sucrose esters acquire specific physical and organoleptic properties of fats. Sucrose esters, with three or less substituted OH groups with fatty acids, are suitable as surfactants and nutritional supplements due to their emulsification, stabilizing and conditioning properties. The main problem with the synthesis of sucrose esters relates to the high functionality of the sucrose molecule - eight hydroxyl groups that compete during the synthesis and lead to the formation of mixtures of monoesters, diesters and even higher esters. Transesterification can be oriented to a specific substitution model by carefully selecting the reaction conditions. Therefore, the focus of this study was to clarify the effects of the sucrose to fatty acid molar ratio, catalyst and reaction temperature on the rate of sucrose ester formation in a specific substitution mode (monoesters). Keywords: sucrose, transesterification, ultrasound synthesis, sucrose esters. INTRODUCTION rate of chemical reactions in solution through the phe- nomenon of cavitation and the generation of microbub- The interest in sucrose esters, which are surfactants bles. -
Preparation of Sucrose Fatty Acid Esters As Food Emulsifiers and Evaluation of Their Surface Active and Emulsification Properties
280 Grasas y Aceites Vol. 50. Fase. 4 (1999), 280-282 Preparation of sucrose fatty acid esters as food emulsifiers and evaluation of their surface active and emulsification properties By Mohamed G. Megahed National Research Centre, Fats and Oils Department, Dokki, Cairo, Egypt. RESUMEN preparation of these compounds (Weiss et al., 1971, 1972; Bobaiek, 1977; Akoh and Swanson, 1987, Preparación de esteres de ácidos grasos con sacarosa 1989), however others excluded solvents in such como emulsionantes alimentarios y evaluación de sus propiedades superficiales y emulsionantes. preparation (Heesen et al., 1976; Rizzi and Taylor, 1978). Se ha llevado a cabo un método simple para la preparación de es It was planned to use a simple method for teres de sacarosa a partir de ácidos grasos y sacarosa de bajo coste. preparation of emulsifiers from sucrose and different Se han usado ácidos laurico, palmítico y oleíco en su preparación, en fatty acids (lauric, palmitic and oleic) aiming to ausencia de solventes orgánicos. Se obtuvieron rendimientos acepta bles del 86.5%, 87.3% y 88.6% para los ásteres del laurico, palmítico develop and improve the method of the preparation y oleíco respectivamente. of sucrose esters. Therefore, it was objective to En los productos se evaluaron sus balances hidrófilo-lipófilo modify the method of Heesen et al., (1976) for the (HLB), sus propiedades de tensión superficial e interfacial así preparation of sucrose emulsifiers (solvent-free como su estabilidad en emulsiones. Los resultados mostraron que estos esteres de sacarosa exhiben propiedades similares a reaction) by replacing the expensive polyalcohols for las de los compuestos preparados comercialmente.